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dc.contributor.authorKalaga, Sudhakar
dc.date.accessioned2014-12-17T20:26:15Z
dc.date.available2014-12-17T20:26:15Z
dc.date.issued1990-12-01
dc.identifier.urihttps://hdl.handle.net/11244/13958
dc.description.abstractDesalting of Tetraethylene Glycol using ion-exchange was studied. For the study Batch and Column experiments were performed using different ion-exchange resins by changing parameters such as Temperature, Water content, and the order of the the ion-exchange resins used. Based on the experimental results design and cost estimation of a desalting plant operating at temperature of 180�F and 2200F were proposed. This process can also be used for other operating temperatures.
dc.formatapplication/pdf
dc.languageen_US
dc.publisherOklahoma State University
dc.rightsCopyright is held by the author who has granted the Oklahoma State University Library the non-exclusive right to share this material in its institutional repository. Contact Digital Library Services at lib-dls@okstate.edu or 405-744-9161 for the permission policy on the use, reproduction or distribution of this material.
dc.titleDesign and Cost Estimation for Desalting Tetraethylene Glycol Using Ion-exchange�
dc.typetext
osu.filenameThesis-1990-K14d.pdf
osu.accesstypeOpen Access
dc.description.departmentChemical Engineering
dc.type.genreThesis


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